CA1232845A - Chromatography column - Google Patents

Chromatography column

Info

Publication number
CA1232845A
CA1232845A CA000456763A CA456763A CA1232845A CA 1232845 A CA1232845 A CA 1232845A CA 000456763 A CA000456763 A CA 000456763A CA 456763 A CA456763 A CA 456763A CA 1232845 A CA1232845 A CA 1232845A
Authority
CA
Canada
Prior art keywords
stationary phase
sample
column
matrix
chromatographic
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
CA000456763A
Other languages
French (fr)
Inventor
Gordon Leeke
Chaokang Chu
Nils Dailey
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
3M Purification Inc
Original Assignee
Cuno Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Cuno Inc filed Critical Cuno Inc
Application granted granted Critical
Publication of CA1232845A publication Critical patent/CA1232845A/en
Expired legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N30/00Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
    • G01N30/02Column chromatography
    • G01N30/60Construction of the column
    • G01N30/6052Construction of the column body
    • G01N30/6069Construction of the column body with compartments or bed substructure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D15/00Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
    • B01D15/08Selective adsorption, e.g. chromatography
    • B01D15/10Selective adsorption, e.g. chromatography characterised by constructional or operational features
    • B01D15/22Selective adsorption, e.g. chromatography characterised by constructional or operational features relating to the construction of the column
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N30/00Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
    • G01N30/02Column chromatography
    • G01N30/60Construction of the column
    • G01N30/6091Cartridges
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N33/00Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
    • G01N33/26Oils; Viscous liquids; Paints; Inks
    • G01N33/28Oils, i.e. hydrocarbon liquids

Landscapes

  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • Immunology (AREA)
  • Pathology (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)
  • Saccharide Compounds (AREA)

Abstract

ABSTRACT

A chromatography column for effecting chromatographic separation of at least two components of a sample flowing therethrough comprising a housing, at least one solid stationary phase in the housing, comprising, a plurality of layers of sheets of swell-able fibrous matrix having chromatographic function-ality and being effective for chromatographic separat-ion, a spacer means between each fibrous matrix layer for controlling swelling of the matrix and enhancing the distribution of sample flowing through the stationary phase by substantially evenly dispers-ing the sample across the matrix; means for distribut-ing the same through the stationary phase and means for collecting the sample after the the sample has flowed through the stationary phase.

Description

~232~3~S

U.S. 16270/16629 CHROMATOGRAPHY COLUMN

Background of the Is~ven~ion L Field of the Invention This invention relates to a novel molecular separation column, e.g. chromatography column, and more particularly to a novel column using a solid stationary phase in cartridge format.
2. Prior Art .
Chromatography is a general term applied to a wide variety of separation techniques based upon the sample interchange between a moving phase, which can be a gas or liquid, and a solid stationary phase. When gas is the moving phase (or "mobile phase' as referred to in chromatographic terminology), the technique is termed gas chromatography and when liquid is the mobile phase, the technique is termed liquid chromatography.
Separations can be classified into either analytical or preparative depending on the objective. In analytical separations, the objective is high resolution separation, identification and quantification of the various components of a sample mixture In preparative chromatography, on the other hand, the objective is the isolation of pure quantities of the desired constituents in the sample.
The collection of chromatographic column techniques can be classified in several ways and the most fundamental is based on naming the types of phases used. I squid absorption chromatography is used extensively for organic and biochemical analysis. Ion exchange ~232~345 chromatography is a special field of liquid-solid chromatography and is specifically applicable to ionic species. Affinity chromatography is based on the attraction (affinity) of a ligand bonded to the solid stationary phase for a given component of the sample. Liquid-liquid or partition chromatography, involves the use of a thin layer of liquid held in place on the surface of a porous inert solid as the stationary phase.
In the chromatographic process, it is customary to pass a mixture of the components to be resolved in a carrier fluid through a chromatographic apparatus or a separative zone. The separative or resolving zone, i.e. the stationary phase, generally consists of a material referred to as a chromatographic media, which has an active chromatographic sorptive function for separating or isolating the components in the carrier fluid. The separative zone usually takes the form of a column through which the carrier fluid passes.
A major problem in the art of column chromatography is to obtain uniform fluid flow across the column. It has been recognized that the solution to this problem resides in an ability to obtain uniform packing, distribution and density of the chromatographic media within a column. To a large degree the packing problem is surmounted in the laboratory chromatography columns by using columns having a small internal diameter, generally on the order of 1/8 inch to 1 1/2 inches.
In such columns uneven chromatographic fluid flow resulting from 1232~345 nonuniform packing of the chromatographic media is quickly relaxed across the column diameter and does not significantly effect analytical results.
To provide an economically feasible preparative chromatography column, the column diameter must be larger than one inch and preferably on the order of one foot or more. Attempts to scale analytical chromatography columns to a size feasible for preparative and/or production chromatography have met with substantial losses in column efficiency. It has been found that as the column diameter or cross-sectional area is increased, the separation or resolving power of the chromatography column decreases. The resolution losses can be attributed primarily to a lack of effective fluid flow distribution in the column.
Various internal column devices have been proposed to overcome the difficulties of producing large diameter preparative and production chromatography columns. Other approaches have been to provide homogeneous distribution of chromatographic media and maintenance of uniform media density across the column or to develop novel type media and/or packing.
Of recent date the Assignee herein has developed unique chromatographic media, comprising in its physical form a homogeneous fibrous matrix, preferably in sheet form. Such issue chromatographic media are described in the following U.S. patents and patent applications:
U.S. Patent No. 4,384,957 to Crowder, 111 et at;
Canadian Patent No. 1,103,001 entitled "Process For Preparing Zero Standard Serum" to Hour Canadian Patent No. 1,201,072 entitled "Fibrous Media Containing Millim4c~on Sized Particles to Hour Canadian Patent Application Serial No. 432,872 filed July 21/83 entitled "Fibrous Media Containing Millimicron Sized Particles" to Hour Canadian Patent Application Serial No. 447,307 filed February 13/84 entitled "Modified Polysaccharide Supports" to Hour Crowder, III et at describes a chromatography column having a substantially homogeneous stationary phase which comprises a porous matrix of fiber having particulate immobilized therein. At least one of the fiber or particulate is effective for chromatographic separations. Preferably, the stationary phase comprises a plurality of sheets in disc form stacked inside a column. The edges of the discs cooperate with the interior wall of the column to form a substantially fluid tight seal therewith, thus preventing any appreciable skewing or I.

aye by-pass of fluid around the edges of the elements. In its preferred form the fluid tight seal is produced by the hydrophilic swelling of the stationary phase.
Ho 1, 103, 001 describes a method for removing thyroid or steroid hormones from a serum by using a composite sheet, comprising a matrix of self bonding fibers having dispersed therein carbon particles. The sheets are used preferably in the chromatographic column described in Crowder III, et at and are also hydrophilic syllable discs or pads.
Ho 1,201,072 & 432,872 describes a self supporting fibrous matrix having immobilized therein at least about 5% by weight of micro particulate, (average diameter less than I micron), preferably fumed silica or alumina The media is also preferably used in the chromatographic columns disclosed in Crowder, III et at and the solid stationary phase is also hydrophilic syllable.
Ho 447,307 describes a modified polysaccharide material which comprises a polysaccharide covalently bonded to a synthetic polymer.
The synthetic polymer is made from a polymerizable compound which is capable of being covalently coupled directly or indirectly to the polysaccharide and one or more polymerizable compounds. The polymerizable compound contains an ionizable chemical group, a chemical group capable of transformation to an ionizable chemical group or a chemical group capable of causing the covalent coupling of the compound to an affinity ligand or biologically active molecule.
The media is capable of acting as a chromato~raphic support for ion exchange chromatography, for affinity chromatography or as reagents for biochemical reactors. Preferably sheets of this material are loaded into an appropriately sized cylindrical column to form the desired stationary phase in a manner similar to Crowder, 111 et at. The preferred solid stationary phase is also hydrophilic syllable.
All of these media in their preferred embodiment, are fibrous matrices which are hydrophilic syllable, i. e. they tend to swell upon contact with aqueous systems. In a stacked disc type chromatographic column such swelling is useful in assisting producing a fluid tight seal with the interior wall of the column to form a water syllable fit therewith Such a seal prevents skewing or bypass of the fluid around the edges of the elements.
In Ho 447 ,307 it is indicated that the media could be used in a "jelly roll" type column, i.e. a sheet of media spirally wound around a pheromones core to form a cylinder having a plurality of layers around the acts thereof. It was subsequently found that the radial flow of a sample through such a "jelly roll" type solid phase was not evenly distributed, and there was substantial bypass of the fluid around certain areas of the media. It is believed that this is due to the swelling and resulting compression of the chromatographic media upon contact with the fluid flowing there through thus producing an irregular ,. . .

i23~2~45 homogeneity in the solid stationary phase leading to an irregular hydrodynamics profile through the column and consequently to the establishment of preferential hydrodynamics routes which rapidly diminish the efficacy and selectivity of the chromatographic column.
Of additional relevance to this invention are the following references:
Wan et alp Biotechnology and Bioengineering XV, pages 93 (1973), describes the preparation of a "Bio-Catalytic Module" wherein collagen-enzyme membranes are layered on a supporting material, such as cellulose acetate membrane, and coiled around a central rod.
Glass rods are used as spacers, which are so arranged that the distance between them is small enough to prevent the adjacent layers from contacting each other. After coiling the complex membrane upon the spacers the cartridge is then fitted into a plastic shell to form a flow-through reactor configuration. The flow through the column is axial, i.e. the sample flowing through the column contacts the membrane in a cross-flow manner.
Wan et at (page 583) also recognizes that the flow of sample through such a device is mainly parallel to the membrane surface and that some of the enzyme molecules located within the matrix may not be readily accessible. In order to improve the contact efficiency Wan et at suggests that the sample flow through the permeable membrane under hydraulic driving pressure. In this configuration of the reactor a ~32~ 5 filter fabric serves as a backing material which separates successive layers of invertase-collagen membrane, thus preventing overlapping of the membrane layers. A perforated stainless steel tube is used as a central core element which is also used for feeding the sample. A
uniform radial distribution of the substrate is achieved by metering flow through a number of holes drilled ninety degrees (zoo) apart radially along the stainless tube. A spiral reactor configuration is formed by coiling alternate layers of the membrane and backing around the steel tube. The spiral cartridge is fitted into a plexiglass outer shell The plastic housing is affixed to two threaded aluminum end plates. The sample is fed from the central tube while the reaction product is collected through a central port located on the periphery of the reactor shell.
U.S. Patent 3,664,095 to Asker describes a packing material which may be spirally wound around a central axis and used for fluid treatment such as drying, heat exchange, ion exchange, molecular sieve separations and the like. Flow is axially through the apparatus, i.e. parallel to the surface of the packing material.
U.S. Patent No. 3,855,6~1 to Huger describes a preparative and production chromatography column which includes a relatively inert inner core onto which is wound in a spiral pattern a relatively inert sheet of material, such as a synthetic polymeric film. Prior to winding, the film is coated with a chromatographic media. A

1232~3~5 thickness dimension of the chromatographic media is arranged substantially perpendicular to the primary direction of fluid flow through the column, i.e.- flow is axial thereof and thus parallel to the surfaces of the chromatographic media U.S. Patent 4,242,4612 Bartoli et at describes a reactor for effecting enzymic reactions in which the flow of the solution to be treated through the catalytic bed takes place radially. It is preferred to have the catalytic bed in the form of coils of enzyme-occluding fibers. The catalytic bed is formed by winding fibers on which the enzymes are supported, so as to form coils with filaments or groups of filaments arranged helically. The fibers inserted in the reactor, can also support, instead of enzymes, chelation agents, antibodies, or similar products which are immobilized, like the enzymes, by physical bonds, ion exchange, absorption, or occlusion in the filamentary polymeric structures.
U.S. Patent 4,259,186 to Boeing et at (1981) describes an elongated gel filtration column having an outer wall and at least one gel chamber defined therein and adapted to be filled with a filter gel.
The gel chamber is sub-divided by a plurality of interior partition walls arranged parallel to the column wall. The partition walls are of a length shorter than the length of the gel chamber.
U.S. Patent 4,299,702 to Byron et at (1981) describes a liquid separation apparatus of the spiral type employing semi-permeable 123Z~3~5 .

-10_ membrane sheets, between which a spacing layer is located, and utilizing the principal of reverse osmosis or ultra filtering for separating a desired liquid component, i.e. a solvent or a solute, from a pressurized feed solution. In this type of apparatus the feed flows substantially spirally through the apparatus, i e. parallel to the mom-brine. See also U S. Patent 4,301,013 to Swept et at (1981).
None of these references describe the problems associated with the use of a syllable fibrous matrix chromatographic media in sheet form utilized in a "jelly roll" type column nor the solution to such problems.

,,, Jo , ,' ' '' ' .

~23Z~345 OBJECTS AND Salem OF THE INVENTION
.

It is an object of this invention, to provide an efficierlt large diameter, preparative or production chromatography column using a solid stationary phase Waco is in cartridge form.
Another object of this invention to provide a solid stationary phase of a chromatography column which can be made in cartridge form.
A further object of this invention to provide a chromatography column which has a solid stationary phase which provides even distribution of a sample flowing radially through the stationary phase.
Still a further object of this mention to provide a chromatographic column which accommodates a syllable fibrous matrix in sheet form as the solid stationary phase.
Another object of this invention to provide a chromatography column which has a reduced pressure drop, enhanced flow and enhanced absorptive capacity.
A further object of this invention is to provide a chromatography column having essentially no determined diametric size limitation, which can be quickly and relatively inexpensively manufactured.
A still further object of this invention is to provide a chromatography column which resolves the uneven fluid flow problems 1232~345 encountered when attempting to scale up analytical columns to preparative and production columns.
Yet another object of the present invention to provide a solid stationary phase for liquid chromatography which insures that substantially all of the chromatographic media is utilized.
A further object of the invention is to provide an inexpensive, high quality chromatographic column which can be a disposable item in many, perhaps most, commercial processing situations.
The foregoing objects of this invention are accomplished by a chromatography column for effecting chromatographic separation of at least two components of a sample flowing through the column. The column comprises a housing and at least one solid stationary phase within the housing. The stationary phase has chromatographic functionality and is effective for chromatographic separation. Means are provided for radially distributing the sample through the stationary phase and for collecting the sample after the sample has flowed through the stationary phase. The stationary phase comprises:
(a) a syllable fibrous matrix in sheet form having chromatographic functionality and being effective for chromatographic separation, spirally wound around the longitudinal axis of the solid stationary phase to form a plurality of layers around the axis; and 1232~45 (b) a spacer means between each layer for permitting controlled swelling thereof and enhancing the distribution of sample flowing radially through the stationary phase.
The solid stationary phase may be fabricated into a cartridge form for placement in the housing. A
plurality of cartridges may be used either in series or parallel flow configuration in a single housing.
In one aspect of the present invention there is provided a chromatography column for effecting chromatographic separation of at least two components of a sample flowing there through comprising a house in, at least one solid stationary phase in -the housing, comprising a plurality of layers of sheets of syllable fibrous matrix having chromatographic functionality and being effective for chromatographic separation and a spacer means between each said fibrous matrix layer for controlling swelling of the matrix and enhancing the distribution of sample flowing through the stationary phase by substantially evenly dispersing the sample across the matrix means for distributing the same through the stationary phase and means for collecting the sample after the the sample has flowed through the stationary phase.

` ~232845 BRIEF DESCRIPTION OF THE DRAWING
Further, characteristics features and advantages of the invention, as well as other objects and usefulness will become readily apparent to those skilled in the art from consideration of the invention as described herein and illustrated by the following drawings:
Figure l. is a partial sectional view of a side elevation of a preferred embodiment of the chromatography column of this invention;
Figure 2. is an enlarged cross-sectional view taken along line 2-2 of figure l;
Figure 3. is a perspective view of a portion of the solid stationary phase broken away therefrom showing the spirally wound chromatographic media and spacer means there between.

123~845 DETAILED DYES ON OF THE INVENTION

The solid stationary phase utilized in this invention comprises a syllable fibrous matrix in sheet form. Preferably, this sheet is homogeneous or substantially homogeneous, which in effect means that the stationary phase is of a uniform or substantially uniform structure and/or composition transverse or axial to the radially flowing sample.
Referring to the drawings, wherein like character references indicate like parts Figures 1 through 3 depict a preferred embodiment of the chromatography column of this invention. Referring to Fig. 1, the column, generally designated 10, is comprised of a cylindrical stationary phase 12, preferably in cartridge form, and a cylindrical chamber I which acts as a housing for the stationary phase 12. The solid stationary phase 12 can be inserted into a glass, metal or polymeric tube or cylinder chamber 14 having a diameter somewhat larger than the external diameter of the stationary phase 12. Suitable fluid admission, collection and monitoring systems can also be employed with the column as in conventional analytical and preparative columns. The stationary phase 12 is positioned within the chamber 14 and preferably has a longitudinal axis 16 co-axial with the axis of the cylindrical chamber 14. Optionally, a plurality of i232~

cartridges 12 may be placed in a single housing in various configurations to effect parallel and/or series flow between the cartridges (not shown). The solid stationary phase has chromatographic functionality and is effective for chromatographic separation. Referring to Figs. 2 and 3, the stationary phase 12 is constructed of a syllable fibrous matrix, usually hydrophilic syllable in sheet form 18 which is the active media for chromatographic separation. The chromatographic media in sheet form 18 is sandwiched between a scrip layer 20 of porous wettable fabric type material of, for example, polyester woven netting, and a non-woven mesh 22. The composite sheet of chromatography media 18, layer of scrip 20 and mesh 22, preferably non-woven, is spirally wound around a pheromones cylindrical core 24 having a longitudinal axis 16, to form a plurality of layers around the axis 16. The mesh 22, due to the openness and thickness thereof, acts as a spacer means between each layer of media 18 which permits the controlled expansion of the syllable media 18 without closing off the porous structure of the media and enhances the distribution of the sample flowing through the stationary phase 12. The cylindrical core 24 is provided with apertures 26 for the flow of sample into the open interior of the core 24.
Referring to Fig. 1, the wound composite sheet, 18, 20 and 22 and core 24 are then slipped into an outer cylindrical member 28 which lZ32845 is also provided Vito apertures 30. The ends of the cylinders are then capped by end caps 32 and I The end caps 32 and 34 are sealed by thermoplastic fusion to the outer cylindrical member 28 and also to the ends of the composite 18, 20 and 22. The fluid or sample 42 can thus flow radially from the outside to the interior of the solid stationary phase, i.e. the open interior of core 24, since the interior and exterior are completely separated by the solid stationary phase and sealed off by end caps 32 and 34 The preformed end caps 32 and 34 are preferably applied to the cylindrical solid stationary phase 12 by heating an inside face of the thermoplastic end cap to a temperature sufficient to` soften and preferably not liquefy, a sufficient amount of the end cap to form a thermoplastic seal with the end of the cylinder 28. All of the edges of one end of the cylinder 28 are then embedded into the softened material. The softened material is then hardened, typically by ambient conditions, to form a thermoplastic sealing relationship between the sealing surface of the end caps 32 and 34, the cylinder 28 and the ends of the solid stationary phase 12 to form a leak-proof seal.
Such methods of applying end caps are well known in the filtration art, see for example, Canadian Patent No. 1,200,766 and Canadian Patent No. 1,184, 512 to Metering et at and Miller, respectively. Optionally, the end caps can be molded integrally in-situ onto the solid stationary phase .

~Z3Z~5 End caps of thermoplastic materials are preferred because of the ease of bonding, but it is also possible Jo use thermo-setting resins in a thermoplastic, fusible or heat soft enable stage of polymerization, until the bonding have been effected, after which the curing of the resin can be completed to produce a structure which can no longer be separated. Such a structure is aye oclavable without danger of destroying the fluid tight seal between the cylinder 28, the solid stationary phase 12 and the end caps 32 and 34. Thermoplastic resins whose softening point is sufficiently high so that they are not softened under sterilizing auto-claving conditions are preferred for biomedical use. Exemplary of the plastic materials which can be used are polyolefins.
Referring to Fig. 1 the preferred cartridge 40 has an end cap 34 on one end which does not open to the exterior of outer cylindrical member 28 but is closed off. This end cap 34 can nest on the bottom end wall I of cylindrical housing I while still permitting the flow of sample 42 into the chamber 14 around the outside of outer cylindrical chamber 28, or this lower end cap 3q of cartridge 40 is in spaced apart relationship from the bottom end wall 44 of cylindrical chamber 14, thus permitting the flow of sample 42 into the chamber 14.
The upper end of cartridge 40 has an end cap 32 which is in fluid communication with cylindrical core 24 thus permitting the flow of fluid from the center of cylindrical core 24 to the outside of end cap 32. A fitting 48, is inserted into end cap 32 so that it may engage the end wall I of cylindrical chamber 14. This fitting may be threaded (as shown) or separately or integrally molded with the end cap and having o-ring seals thereon. End wall 46 has thereon a threaded nipple SC which permits the flow of treated sample 42 to pass from the core 24 through end cap Andy end wall 46 into the process stream for additional processing. The end wall 46, and optionally end wall I may be threadedly attached to the wall 52 of cylindrical chamber 14 or easy access to the interior for cleaning and insertion of the cartridge I
The present invention as conceived utilizes known media and known media preparation techniques, specifically those described in the aforementioned co-pending applications and patents. This preferred media is fibrous, in sheet form and generally has the characteristics that it is hydrophilic syllable. The preferred chromatographic media is that described in the aforementioned Crowder, III et at patent, and Ho patents and applications.
It should be realized however that this invention is applicable to any type of syllable media in sheet form, whether it is hydrophilic syllable or otherwise.
In order to provide a chromatographic media matrix which is coherent and handle able, it is desirable that at least one of the components which go into forming the porous matrix be a long, self I.,, 1232~3~S

bonding structural fiber. Such fiber gives the stationary phase sufficient structural integrity in both the wet "as formed" condition and in the final dry condition. Such a structure permits handling of the phase, in particular a sheet, during processing and at the time of its intended use. Preferably the sheets which form the chromatographic media are formed by vacuum felting an aqueous slurry of fibers. The sheets may also be pressure felled or felled from a non-aqueous slurry. The sheet shows a uniform high porosity, with excellent flow characterics and is substantially homogeneous. In general, the media can range in thicknesses of from about 5 miss to about 30 miss (dry), however thicker or even thinner media may be utilized provided the sheet can be spirally wound to produce a cartridge which can perform as described herein. The media can swell to at least 25% this thickness, and generally greater, e.g. two to four times this thickness.
It is important when constructing the chromatography column of this invention that the chomatographic media used in the column be of uniform thickness throughout its length and width and that the media have a substantially uniform density throughout. It is preferred that the layer of media be substantially homogeneous with respect to itself, however, for certain applications and material it is to be understood that nonhomogeneous construction may be employed.

Sue Since the solid stationary phase is intended in use to effect separation by maintaining a substantial pressure differential across the solid stationary phase, it is essential that the solid stationary phase have a sufficient degree of compressive strength to withstand deformation under such loads as may be imposed upon it. Such compressive strength must not only exist in the media itself but in the spacer means and the internal core upon which the chromatography media, or solid stationary phase is compressed.
Due to the sealability of the media, a key element of this invention is the spacer means between each layer of the media The spacer means permits controlled expansion of the media and enhancement of the distribution of sample flowing through the stationary phase. The spacer means located between each layer of the syllable chromatographic media provides for the axial and the circumferential movement of the sample as the sample passes radially through the solid stationary phase. The spacer means functions to ~miiEormly control thickness and density of the chromatographic media during use . In addition, the spacer means can serve as a backing or support for the layer of chromatographic media. This latter aspect is particularly useful during the manufacturing phase.
It is preferred that the spacer means be composed of a material which is inert with respect to the chromatographic process. By inert ~32~;L5 it is meant the material does not adversely effect the function of the solid stationary phase.
Referring lo Figs. 2 and 3, the spacer means may comprise two elements thereof, i.e. the scrip 20 and the mesh 22. The scrip material 20 functions to channel, to a certain extent, the sample flowing through the media and substantially evenly disperse the sample axially and circumferential across the media. The mesh material provides spacing between the media to permit controlled expansion thereof to prevent the "cutoff" of flow there through by compression of the permeable media and also assists in distributing or channeling the sample flowing radially through the media both axially and circumferential.
The scrip 20 is preferably a porous material which is wettable by the sample to maximize the distribution of sample during flow through the stationary phase. Such wettable scrims can, for example, be made of non-woven textiles and cloth, papers and similar materials.
Suitable wettable scrims include polyester non-woven fibrous webs or woven webs, using mono-filaments or multi-filament yarn, the moo-filaments being preferred in terms of open structure and lower pressure drops, polyamide fiber woven webs, woven and non-woven webs of aromatic polyamides, and other relatively fibrous products such as cellulose, regenerated cellulose, cellulose esters, cellulose esters, glass fiber, and similar materials. Cellulosic and synthetic lZ3284S

fiber filter papers may also be used as the scrip material as well as perforated plastic sheets and open mesh expanded plastics. These latter more open type scrims merge, to a certain extent, into the mesh spacer material in function. It is conceivable that the function of the scrip and mesh may be combined into one type material of proper nettability and pore structure to function in distributing the sample flowing through the stationary phase both axially and circumferential while still permitting controlled expansion of the media to allow the passage of the sample there through to the next layer of media, for example, a porous compressible spongelike material.
More specifically preferred scrims are polyester spun bonded non-woven webs trademarked ROME from Dupont Eaton Dike Mann Charles, HOLLYTEX; polyprowlene webs such as HOLLYTEX; Kendall Corps NOVONETTE Crown Zellerbach's" .75 ozlsq. ye.; and Kendall's WEBRIL; Lutravil Sales Co's. LUTRASIL and Shakeup Mills' VISION may also be used.
The mesh material is a more open type of material having openings ranging, for general guidance, from l/16 inch to a I inch and is at least equivalent in thickness to the thickness of the media.
It should be noted that the thickness of the spacer means, i.e.
the scrip and particularly the mesh material, and the pore size of SLY

each to be used may be readily determined by cone skilled in the art by performing tests which vary these factors. Such factors as the openness and thickness of these spacer means are highly dependent on the type of media utilize, e.g. sealability, nettability, thickness, chemical composition, etc., the flow rate of the sample through the stationary phase, the surface area of the stationary phase, e.g. member of windings, thickness of media, diameter of stationary phase, etc. It is thus very difficult to clearly specify these variables, other than to X
say that these may be determined by either trial and error or more elaborate testing procedures to determine the optimum parameters.
For general guidance, it has been found that a scrip material having a thickness of from about 5 Mulls to about 10 miss and mesh having a thickness of from about 5 miss to about 30 miss and openings of about 1/16 to about inch is suitable.
The preferred scrip material, at this time, is polyester Rome Grade 2014.
The preferred mesh material, at this time, is polypropylene COWED (GRADE TD-620).
Referring to Fig. 2, after winding the chromatography media 18 on the core 24, the exterior surface thereof is completely wrapped with the scrip material 20.
The overall width of the stationary phase in accordance with the present invention can be infinite, the actual diameter being limited only by practical considerations such as space requirements.
Since the diameter or width of the overall column can be increased without theoretical limitation, the sample size or amount of substance to be separated in the bed is not limited. Thus the diameter can be increased to separate the desired amount of sample substance to be produced.
In operation, the sample is driven radially through the stationary phase and separated into distinct chromatographic fractions by the chromatographic media. The spacer means induces and permits circumferential and axial flow of this stream as it moves through the column and therefore provides for improved resolution and utilization of the medics potential capacity.
Referring to Fig. 1, the sample is preferably introduced at the bottom of the column flowing to the outer surface of the solid stationary phase and then flowing radially inwardly through the layers of chromatographic media and spacer means into the perforated central tube 24 and is withdrawn centrally. It is apparent, from what has been set forth above that the radial flow can also be caused to circulate in the opposite direction.
The chromatographic columns of this invention may be used for any of the well-known chromatographic separations usually performed with conventional columns. Additionally, the columns of the present 1~32~3~5 invention may be found useful in the areas where conventional columns are impractical.
The novel columns of this invention can be used for separations in the analytical and preparative fields. The columns can be connected to all common types of chromatographic equipment.
Several columns or cartridges of solid stationary phase can be connected in series or parallel. In large units, the columns can contain identical or different chromatographic media and can be of identical or different length and/or diameter.
It has been found that the aforediscribed cartridge 40 when used in conjunction with housing 14 produces unexpected results in that the flow of sample through the column is enhanced without destroying the absorptive capacity of the media Additionally when protein and dye staining tests were performed it was found that the solid stationary phase of this invention provided even distribution of sample flow there through without an increase in pressure drop when compared to a spirally wound cartridge not utilizing the spacer means described herein.
From the foregoing it can be seen that a convenient cartridge configuration has been invented which is easy to install, operate, and disassemble and is easily adaptable to any batch size or continuous type operation by the use of multiple configurations. Additionally the chromatography column cartridge has excellent structural integrity.

The cartridges decrease total processing time and when used with the proper chromatographic media has excellent binding capacity.
The cartridges may be used with standard type pumps or gravity feed and utilized, in their preferred mode, at from S to 50 PSI. The cartridges of chromatographic media are totally enclosed and completely self contained to ensure sterile conditions. Due to the fact that the solid stationary phase cartridge is manufactured in a factory and assembled therein each cartridge is virtually identical to the other, does not vary as in previously known columns and eliminates the dependence upon packing expertise. Additionally there is no pro-measuring of chromatographic media, no media loss due to handling, no packing problems, no fines generation and removal within the column and other problems associated with packing chromatographic cartridges. The column is simple to operate, does not produce any channeling by passing or shifts in bed volume. The chromatographic cartridges allow scale up from milligram laboratory quantities to megagram production quantities. The cartridge provides rigidity and strength and are particularly useful as a high flow medium pressure matrix and is highly suitable for large scale protein or non-protein purifications.
The present invention has been described in relation to several embodiments. Upon reading the specification one of ordinary skill in the art would be able to effect various alterations or, changes in or 1;~321~45 substitutions of equivalence to the present invention as disclosed. It is intended thaw the invention as conceived be limited only by the definition of the invention contained in the appended claims.

issue SUPPLEMENTARY DISCLOSURE
This supplementary disclosure relates to a chromatography column for effecting chromatographic separation of at least two components of a sample flowing there through. It more particularly relates to a further preferred embodiment according to the present invention, to that disclosed in the principal disclosure.
In a drawing which illustrates the further preferred embodiment of the invention according to the supplementary disclosure:
Figure 4 is a partial sectional view of a side elevation of the embodiment of the chromatography column of this invention;
Figure 5 is an enlarged cross-sectional view taken along line 5-5 in Figure 4; and Figure 6 is a perspective view of the core with a portion of the solid stationary phase broken away therefrom showing the spirally wound cremate-graphic media and spacer means there between.
The solid stationary phase in this embody-mint comprises a syllable fibrous matrix in sheet form. Preferably, this sheet is homogeneous or sub-staunchly homogeneous, which in effect means that the stationary phase is of a uniform or substantially uniform structure and/or composition.
Referring to the drawings, wherein like character references indicate like parts, Figures 4 through 6 depict the embodiment of the chromatography column of this invention. Referring to Figure 4, the column, which may be in cartridge form, generally designated 10, is comprised of a cylindrical stay shunner phase 12, and cylindrical tube 13, which form a cylindrical chamber 14 which acts as a housing for the stationary phase 12. The solid stationary phase 123284~

12 can be inserted into chamber 14 formed by a glass, metal or polymeric tube or cylinder 13 having a diameter somewhat larger than the external diameter of the stationary phase 12. Suitable fluid admission, collection and monitoring systems can also be employed with the column as in conventional analytical and preparative columns. The stationary phase 12 is positioned within the chamber 14 and preferably has a longitudinal axis 16 coaxial with the axis of the cylindrical chamber 14. Optionally, a plurality of cartridges may be placed in a single housing in various configurations to effect parallel and/or series flow between the cartridges (not shown). The solid stationary phase has chromatographic function-amity and is effective for chromatographic separation.
Referring to Figures 5 and 6, the stationary phase 12 is constructed of a syllable fibrous matrix 18, usually hydrophilic syllable, in sheet form which is the active media for chromatographic separation.
The chromatographic media in sheet form 18 is sand-wicked between a single non-woven mesh 22 or plurality of mesh. The composite sheet of chromatography media 18 and mesh 22, preferably non-woven, is spirally wound around a cylindrical core 24 having a long-tudinal axis 16 to form a plurality of layers around the axis 16. The core 24 is provided with a plurality of longitudinal and axially oriented channels 21 for directing the liquid into circumferential channels 23 which are in fluid communication with core 24. The mesh 22, due to the openness and thickness thereof, acts as a spacer means between each layer of media 18 which permits the controlled swelling of the media and enhances the distribution of the sample flowing through the stationary phase 12. The cylindrical core ,~,,, lZ328~5 24 is provided with apertures 26 near the top thereof for the flow of sample from the circumferential channels 23 in the open interior of the core.
Referring to Figure 4, the wound composite sheet 18 and 22 and core 24 are then capped by stay shunner phase end caps 32 and 34. The stationary phase end caps 32 and 34 of this subassembly are sealed by thermoplastic fusion to the core 24 and also to the ends of the composites 18 and 22. The subassembly, comprising 18, 22, 24, 32 and 34 is then slipped into chamber 14. The cylinder end cap 36 is then thermos plastically fused to the top edge 31 of cylinder 13.
The fluid or sample 42 can thus flow radially from the outside through the solid stationary phase to the open channel 21 of core 24, since the interior and exterior are completely separated by the solid stationary phase and sealed off by stationary phase end caps 32 and 34.
The preformed stationary phase end caps 32 and 34 are preferably applied to the cylindrical solid stationary phase 12 by heating an inside face of the thermoplastic stationary phase end cap to a temper-azure sufficient to soften a sufficient amount of the stationary phase end cap to form a thermoplastic seal with the ends of the core 24 and composite sheet 18 and 22. All of the edges are then embedded into the softened material. The softened material is then hardened, typically by ambient conditions, to form a thermoplastic sealing relationship between the sealing surface of the stationary phase end caps 32 and 34, the core 24 and the ends of the solid stationary phase 12 to form a leak-proof seal. Such methods of applying stationary phase end caps are well known in the filtration art. See, for example, U.S. serial no.
383,383 and U.S. serial no. 383,377, filed on May 28, 1982, to Mirroring et at and Miller, respectively.

~23;~845 Optionally, the stationary phase end caps can be molded integrally in situ onto the solid stationary phase.
Stationary phase end caps of thermoplastic materials are preferred because of the ease of bond-in, but it is also possible to use thermo-setting resins in a thermoplastic, fusible or heat-softenable stage of polymerization, until the bonding have been effected, after which the curing of the resin can be completed to produce a structure which can no longer be separated. Such a structure is autoclavable without danger of destroying the fluid tight seal, the solid stationary phase 12, and the stationary phase end caps 32 and 34. Thermoplastic resins whose softening point is sufficiently high so that they are not softened under sterilizing autoclaving conditions are preferred for biomedical use. Exemplary of the plastic ma-trials which can be used are polyolefins.
Referring to Figure 4, the preferred column 10 has a stationary phase end cap 34 on one end which does not open to the exterior of the subassembly 18, 22, 24, 32, and 34 but is closed off. This stationary phase end cap 34 can nest on the bottom end wall 44 of cylinder 13 while still permitting the flow of sample 42 into chamber 14 around the outside of stationary phase 12, or this lower stationary phase end cap 34 of the subassembly 18, 22, 24, 32 and 34 is in spaced apart relationship from the bottom end wall 44 of cylinder 13, thus permitting the flow of sample 42 into the chamber 14.
The upper end of cartridge 40 has a cylinder end cap 36 which is in fluid communication with channels 21 of cylindrical core 24 thus permitting the flow of fluid from the outer periphery of cylindrical core 24 to the center of core 24 to the outside of lZ3;~845 cylinder end cap 36. The cylinder end cap 36 has molded thereon fitting 48 for fluid connection through a collection means (not Sheehan Referring to Figure 5, prior to winding the chromatography media 18 on the core 24, the exterior surface of core 24 may be completely wrapped with a scrip material 20. Additionally, after winding the chromatography media 18 on the core 24, the exterior surface thereof may be completely wrapped with mesh material 22.
Preferably, the sheets which form the chromatographic media are formed by vacuum felting an aqueous slurry of fibers. The sheets may also be pressure felled or felled from a non-aqueous slurry.
The sheet shows a uniform high porosity, with ox-silent flow characteristics, and is substantially homogeneous. In general, the media can range in thicknesses from about 5 miss to about 150 miss (dry);
however, thicker or even thinner media may be utilized provided the sheet can be spirally wound or layered to produce a column which can perform as described above.
Due to the sealability of the cremate-graphic media used in the chromatography column of the invention, a key element of this invention is the spacer means between each layer of the media and/or the coxswain of the chamber wall and the fibrous matrix.
Having further reference to Figures 5 and 6, the spacer means comprises the mesh 22.
The mesh material provides spacing between the media to permit controlled expansion thereof to prevent the "cut-off" to flow there through by come press ion of the permeable media and also assists in distributing or channeling the sample flowing radially through the media both axially and circumferential.

~Z32845 As in the case of applicant's other disk closed embodiments, the mesh material is an open type of material having openings ranging, for general guidance, from 1/16" to 1/4".
In operation, the sample is driven through the stationary phase and separated into distinct chromatographic fractions by the chromatographic media. The spacer means induces and permits flow of this stream as it moves through the column and there-fore provides for improved resolution and utilization of the media's potential capacity.
Referring to Figure 4, the sample is pro-fireball introduced at the bottom the column flowing to the outer surface of the solid stationary phase and then flowing radially inward through the layers of chromatographic media and spacer means into the channels 21 of core tube 24 and is withdrawn central-lye It is apparent, from what has been set forth above, that the radial flow can also be caused to circulate in the opposite direction.
It has been found that the aforedescribed stationary phase produces unexpected results in that the flow of sample through the column is enhanced without destroying the adsorptive capacity of the media. Additionally, when protein and dye staining tests were performed it was found that the stationary phase of this invention provided even distribution of sample flow there through without an increase in pressure drop when compared to a stationary phase not utilizing the spacer means described herein.
From the foregoing, it can be seen that a convenient stationary phase configuration has been invented which is easy to install, operate, and disassemble and is easily adaptable to any batch size lZ32845 or continuous type operation by the use of multiple configurations. Additionally, the chromatography column has excellent structural integrity.
The stationary phases decrease total pro-cussing time and when used with the proper cremate-graphic media has excellent binding capacity. The stationary phases may be used with standard type pumps, gravity feed, or syringes, utilized, in their preferred mode, at from 1 to 50 psi, and even under vacuum. The stationary phases of chromatographic media are totally enclosed and completely self-contained to ensure sterile conditions. Due to the fact that the solid stationary phase is manufactured in a factory and assembled therein, each is virtually identical to the other, does not vary as in previously known columns and eliminates the dependence upon packing expertise. Additionally, there is no remeasuring of chromatography media, no media loss due to handling, no peeking problems, no fines generation and removal within the column and other problems associated with packing ehromatographic columns. The column is simple to operate, does not produce any channeling by passing or shifts in bed volume. The ehromatographic station-cry phase allows scale up from milligram laboratory quantities to megagram production quantities. The stationary phase provides rigidity and strength and is particularly useful as a high flow, medium pressure matrix and is highly suitable for large scale protein or non-protein purifications.

Claims (25)

The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:
1. A chromatography column for effecting chromatographic separation of at least two components of a sample flowing therethrough comprising:
a housing;
at least one solid stationary phase in said housing having a longitudinal axis, said phase having chromatographic functionality and being effective for chromatographic separation;
a means for radially distributing the sample through the stationary phase;
a means for collecting the sample after the sample has flowed through the stationary phase;
wherein the stationary phase comprises:
(a) a swellable fibrous matrix in sheet form having chromatographic functionality and being effective for chromatographic separation, spirally wound around the longitudinal axis of the solid phase to form a plurality of layers around the axis;
(b) a spacer means between each layer for permitting controlled swelling thereof and enhancing the distribution of sample flowing radially through the stationary phase.
2. The column of Claim 1, wherein the housing and stationary phase are cylindrical and coaxial and the housing has a diameter greater than the stationary phase.
3. The column of Claim 1, wherein the swellable matrix swells at least about 35% of its thickness.
4. The column of Claim 1, wherein the swellable matrix is hydrophilic swellable.
5. The column of Claim 1, wherein the matrix is spirally wound around a foraminous cylindrical core.
6. The column of Claim 5, wherein the foraminous cylindrical core is in fluid communication with the means for collection.
7. The column of Claim 5, wherein the stationary phase is enclosed in an outer cylindrical member having apertures therein.
8. The column of Claim 7, wherein the ends of the stationary phase are capped at one end by an end cap which has an opening therein which is in fluid communication with the cylindrical core and at the other end by a solid end cap.
9. The column of Claim 1 wherein the spacer means comprises:
(a) a scrim layer for channelling the sample flow through the matrix and substantially evenly dispersing the sample axially and circumferentially across the matrix; and (b) a mesh layer to provide a spacing between the layers to permit controlled expansion thereof and assist in distributing the sample axially and circumferentialy across the matrix.
10. The column of Claim 9, wherein the scrim layer completly covers the exterior surface of the solid stationary phase.
11. The column of Claim 1 or 8 wherein the solid stationary phase is a disposable cartridge.
12. A solid stationary phase having a longitudinal axis, said phase having chromatographic functionality and being effective for chromatographic separation, wherein the stationary phase comprises:
(a) a swellable fibrous matrix in sheet form having chromatographic functionality and being effective for chromatographic separation, spirally wound around the longitudinal axis of the solid phase to form a plurality of layers around the axis;
(b) a spacer means between each layer for permitting controlled swelling thereof and enhancing the distribution of sample flowing radially through the stationary phase.
13. The stationary phase of Claim 12, wherein the swellable matrix swells at least about 25% its thickness.
14. The stationary phase of Claim 12, wherein the swellable matrix is hydrophilic swellable.
15. The stationary phase of claim 12, wherein the matrix is spirally wound around a foraminous cylindrical core.
16. The stationary phase of Claim 15, wherein the stationary phase is enclosed in an outer cylindrical member having, apertures therein.
17. The stationary phase of Claim 16, wherein the ends of the stationary phase are capped at one end by an end cap which has an opening therein which is in fluid communication with the cylindrical core and at the other end by a solid end cap.
18. The stationary phase of Claim 12 wherein the spacer means comprises:
(a) a scrim layer for channelling the sample flowing through the matrix and substantially evenly dispersing the sample axially and circumferentially across the matrix; and (b) a mesh layer to provide a spacing between the layers to permit controlled expansion thereof and assist in distributing the sample axially and circumferentially across the matrix.
19. The stationary phase of Claim 18, wherein the scrim layer completly covers the exterior surface of the solid stationary phase.
20. The stationary phase of Claim 12 or 17 which is a disposable cartridge.
21. A chromatography column for effecting chromatographic separation of at least two components of a sample flowing therethrough comprising:
a housing;
at least one solid stationary phase in said housing, comprising:
(a) a plurality of layers of sheets of swellable fibrous matrix having chroma-tographic functionality and being effective for chromatographic separa-tion, and (b) a spacer means between each said fibrous matrix layer for controlling swelling of the matrix and enhancing the distribution of sample flowing through the stationary phase by sub-stantially evenly dispersing the sample across the matrix; means for distri-buting the same through the stationary phase; and means for collecting the sample after the he sample has flowed through the stationary phase.

CLAIMS SUPPORTED BY SUPPLEMENTARY DISCLOSURE
22. The column of claim 21 wherein the swellable fibrous matrix is hydrophilic swellable.
23. The column of claim 21 wherein the spacer means comprises:
(a) means for channeling the sample flow through the matrix and substantially evenly dispersing the sample; or (b) means for providing a spacing between the layers to permit controlled expansion thereof and assist in distributing the sample; or (c) (a) in combination with (b).
24. The column of claim 21 wherein the swellable fibrous matrix swells to at least about 25% of its thickness.
25. The stationary phase of claim 23 wherein said means comprises a mesh layer to provide a spacing between the layers to permit controlled expansion thereof and assist in distributing the sample.
CA000456763A 1983-06-17 1984-06-18 Chromatography column Expired CA1232845A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US505,532 1983-06-17
US06/505,532 US4496461A (en) 1983-06-17 1983-06-17 Chromatography column
US723,691 1985-04-16

Publications (1)

Publication Number Publication Date
CA1232845A true CA1232845A (en) 1988-02-16

Family

ID=24010697

Family Applications (1)

Application Number Title Priority Date Filing Date
CA000456763A Expired CA1232845A (en) 1983-06-17 1984-06-18 Chromatography column

Country Status (10)

Country Link
US (2) US4496461A (en)
EP (1) EP0130418B1 (en)
JP (1) JPS60501572A (en)
AU (1) AU578900B2 (en)
BR (1) BR8406929A (en)
CA (1) CA1232845A (en)
DE (1) DE3484946D1 (en)
DK (1) DK74385A (en)
IL (1) IL72037A (en)
WO (1) WO1985000020A1 (en)

Families Citing this family (70)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4639513A (en) * 1984-02-02 1987-01-27 Cuno Inc. Intravenously injectable immunoglobulin G (IGG) and method for producing same
US4743373A (en) * 1983-06-17 1988-05-10 Cuno Incorporated Chromatography column
US4986909A (en) * 1983-06-17 1991-01-22 Cuno Incorporated Chromatography column
US4496461A (en) * 1983-06-17 1985-01-29 Amf Incorporated Chromatography column
US4606824A (en) * 1984-10-26 1986-08-19 Chaokang Chu Modified cellulose separation matrix
US4882047A (en) * 1985-03-22 1989-11-21 Ht Chemicals, Inc. Zero-void column end plate for chromatography
US4627918A (en) * 1985-11-04 1986-12-09 Sepragen Corporation Chromatography column using horizontal flow
US4840730A (en) * 1986-07-25 1989-06-20 Sepragen Corporation Chromatography system using horizontal flow columns
US4927540A (en) * 1986-09-04 1990-05-22 The Dow Chemical Company Ionic complex for enhancing performance of water treatment membranes
US5013433A (en) * 1987-01-21 1991-05-07 H.T. Chemicals, Inc. Zero void column end plate for chromatography
US4995163A (en) * 1987-04-22 1991-02-26 The Perkin-Elmer Corporation Method of assembling a chromatography column
US4872979A (en) * 1987-04-22 1989-10-10 The Perkin-Elmer Corporation Chromatography column
US4833083A (en) * 1987-05-26 1989-05-23 Sepragen Corporation Packed bed bioreactor
US4894152A (en) * 1987-08-13 1990-01-16 Cerex Corporation Fluid control device
US4891133A (en) * 1987-09-15 1990-01-02 Cerex Corporation Chromatography apparatus
DE3738691A1 (en) * 1987-11-13 1989-05-24 Chmiel Horst METHOD AND DEVICE FOR PREPARATIVE LIQUID CHROMATOGRAPHY OR ADSORPTION
AU3047989A (en) * 1988-02-11 1989-09-06 Cuno Incorporated Affinity matrices of modified polysaccharide supports
US4969995A (en) * 1988-08-26 1990-11-13 The United States Of America As Represented By The United States Department Of Energy Removal of metal ions from aqueous solution
CH676799A5 (en) * 1988-11-01 1991-03-15 Sulzer Ag
US4957620A (en) * 1988-11-15 1990-09-18 Hoechst Celanese Corporation Liquid chromatography using microporous hollow fibers
US5019270A (en) * 1989-07-06 1991-05-28 Perseptive Biosystems, Inc. Perfusive chromatography
US5228989A (en) * 1989-07-06 1993-07-20 Perseptive Biosystems, Inc. Perfusive chromatography
US5242384A (en) * 1989-11-13 1993-09-07 Davol, Inc. Blood pumping and processing system
DE4119203A1 (en) * 1990-08-07 1992-02-13 Bio Rad Laboratories CHROMATOGRAPHY INSERT
US5169522A (en) * 1990-09-25 1992-12-08 Ht Chemicals, Inc. Column slurry packing compressor
JPH06508792A (en) * 1991-06-28 1994-10-06 ミネソタ マイニング アンド マニュファクチャリング カンパニー Products for separation and purification and methods for adjusting their porosity
US5248428A (en) * 1991-06-28 1993-09-28 Minnesota Mining And Manufacturing Company Article for separations and purifications and method of controlling porosity therein
JPH07198701A (en) * 1993-11-26 1995-08-01 Ngk Insulators Ltd Column and column device for low-pressure high-precision liquid chromatography and method for using column device
DE9405378U1 (en) * 1994-03-30 1994-06-23 Hewlett-Packard GmbH, 71034 Böblingen Separation column for chromatography
WO1996029146A1 (en) 1995-03-22 1996-09-26 Minnesota Mining And Manufacturing Company Solid phase extraction membrane
US5897779A (en) * 1997-02-13 1999-04-27 Minnesota Mining And Manufacturing Company Spiral wound extraction cartridge
DE19711083C2 (en) * 1997-03-18 1999-04-29 Sartorius Gmbh Device and method for adsorptive material separation with adsorption membranes
WO2003008063A2 (en) * 2001-07-17 2003-01-30 Hti Filtration Corporation Filter for oils containing adhesive contaminants
US20090056541A1 (en) * 2001-08-01 2009-03-05 Davison Dale A Method and apparatus for high resolution flash chromatography
US20050242018A1 (en) * 2001-08-01 2005-11-03 Teledyne Isco, Inc. Disposable chromatographic columns
US7261812B1 (en) 2002-02-13 2007-08-28 Nanostream, Inc. Multi-column separation devices and methods
EP1474236B1 (en) * 2002-02-13 2006-01-04 Nanostream, Inc. Microfluidic separation column devices and fabrication methods
US7028536B2 (en) * 2004-06-29 2006-04-18 Nanostream, Inc. Sealing interface for microfluidic device
US6923908B1 (en) * 2003-10-17 2005-08-02 Systec, Llc Filter apparatus
EP2821135A1 (en) * 2004-02-05 2015-01-07 EMD Millipore Corporation Porous adsorptive or chromatographic media
WO2005078016A1 (en) * 2004-02-05 2005-08-25 Millipore Corporation Room temperature stable agarose solutions
EP1711250A1 (en) 2004-02-05 2006-10-18 Millipore Corporation Method of forming coated structures
US7479223B2 (en) * 2004-02-05 2009-01-20 Millipore Corporation Porous adsorptive or chromatographic media
WO2005078028A1 (en) * 2004-02-05 2005-08-25 Millipore Corporation Method of forming polysaccharide structures
US7481917B2 (en) * 2004-03-05 2009-01-27 Hydranautics Filtration devices with embedded radio frequency identification (RFID) tags
US7138061B2 (en) * 2004-05-10 2006-11-21 Scientific Plastic Products, Inc. Flash chromatography cartridge
WO2007030647A2 (en) * 2005-09-07 2007-03-15 Hydranautics Reverse osmosis filtration devices with rfid tag-powered flow and conductivity meters
WO2007108977A2 (en) * 2006-03-13 2007-09-27 Hydranautics Device for measuring permeate flow and permeate conductivity of individual reverse osmosis membrane elements
US7844070B2 (en) * 2006-05-30 2010-11-30 Sonitus Medical, Inc. Methods and apparatus for processing audio signals
US7641860B2 (en) * 2006-06-01 2010-01-05 Nanotek, Llc Modular and reconfigurable multi-stage microreactor cartridge apparatus
AU2007258799B2 (en) * 2006-06-14 2012-02-02 T.L.X Extraction Technologies Limited Method and apparatus for liquid-liquid extraction
EP2160226B1 (en) * 2007-06-27 2015-11-11 GE Healthcare Bio-Sciences Corp. System and method for assembling a large scale chromatograpy structure
US9433922B2 (en) * 2007-08-14 2016-09-06 Emd Millipore Corporation Media for membrane ion exchange chromatography based on polymeric primary amines, sorption device containing that media, and chromatography scheme and purification method using the same
US20090130738A1 (en) * 2007-11-19 2009-05-21 Mikhail Kozlov Media for membrane ion exchange chromatography
US8636957B2 (en) * 2009-05-07 2014-01-28 Southwest Research Institute Spiral, microchanneled chromatographic column and detection systems
GB0922426D0 (en) 2009-12-22 2010-02-03 Ge Healthcare Bio Sciences Ab Containers for chromatography media
KR101871683B1 (en) 2010-07-30 2018-06-27 이엠디 밀리포어 코포레이션 Chromatogrphy media and method
WO2012018294A1 (en) 2010-08-05 2012-02-09 Ge Healthcare Bio-Sciences Ab Method for storage and stabilization of a target substance
AU2013330344B2 (en) 2012-09-17 2018-07-05 W. R. Grace & Co.-Conn. Chromatography media and devices
US9486717B2 (en) 2014-03-13 2016-11-08 Folim G. Halaka Purification columns and methods
EP3117208A4 (en) 2014-03-13 2018-01-24 Folim G. Halaka Purification columns and methods
US11680080B2 (en) 2014-03-13 2023-06-20 Folim G. Halaka Purification columns and methods
JP6914189B2 (en) 2014-05-02 2021-08-04 ダブリュー・アール・グレース・アンド・カンパニー−コーンW R Grace & Co−Conn Functionalized Carrier Materials and Methods for Making and Using Functionalized Carrier Materials
ES2877563T3 (en) 2014-09-02 2021-11-17 Emd Millipore Corp Chromotography media comprising discrete porous arrays of nanofibrils
WO2016093926A1 (en) 2014-12-08 2016-06-16 Emd Millipore Corporation Mixed bed ion exchange adsorber
EP3302784B1 (en) 2015-06-05 2021-10-06 W.R. Grace & Co.-Conn. Adsorbent bioprocessing clarification agents and methods of making and using the same
EP3802993B1 (en) * 2018-06-22 2023-11-08 Zodiac Pool Systems LLC Filters principally for use in connection with swimming pools and spas
CN112955246A (en) * 2018-07-27 2021-06-11 纳米系列有限责任公司 Multi-membrane separation capsule
JP2023528209A (en) * 2020-05-12 2023-07-04 スリーエム イノベイティブ プロパティズ カンパニー Spacer ring for chromatography device
CN115551610A (en) * 2020-05-12 2022-12-30 3M创新有限公司 Membrane seal and spacer ring for a viral clearance chromatographic separation device

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3856681A (en) * 1972-08-17 1974-12-24 C Huber Chromatography apparatus and method
CA1044537A (en) * 1973-05-09 1978-12-19 Amf Incorporated Filter medium and process
US4309247A (en) * 1976-03-15 1982-01-05 Amf Incorporated Filter and method of making same
CA1148872A (en) * 1979-04-06 1983-06-28 Eugene A. Ostreicher Filter with inorganic cationic colloidal silica
EP0046470B1 (en) * 1980-08-22 1984-12-05 The Stolle Research And Development Corporation Hemoperfusion device for specific modification or removal of components of whole blood
US4384957A (en) * 1980-09-08 1983-05-24 Amf Incorporated Molecular separation column and use thereof
US4559145A (en) * 1982-06-16 1985-12-17 Amf Incorporated Process for preparing a zero standard serum
US4496461A (en) * 1983-06-17 1985-01-29 Amf Incorporated Chromatography column

Also Published As

Publication number Publication date
IL72037A (en) 1987-11-30
US4496461A (en) 1985-01-29
IL72037A0 (en) 1984-10-31
WO1985000020A1 (en) 1985-01-03
EP0130418B1 (en) 1991-08-21
JPS60501572A (en) 1985-09-19
DK74385D0 (en) 1985-02-15
JPH0363020B2 (en) 1991-09-27
DE3484946D1 (en) 1991-09-26
AU578900B2 (en) 1988-11-10
EP0130418A2 (en) 1985-01-09
BR8406929A (en) 1985-06-04
AU3070084A (en) 1985-01-11
US4675104A (en) 1987-06-23
EP0130418A3 (en) 1988-04-27
DK74385A (en) 1985-02-15

Similar Documents

Publication Publication Date Title
CA1232845A (en) Chromatography column
US4743373A (en) Chromatography column
US4986909A (en) Chromatography column
US7390403B2 (en) Prefilter system for biological systems
US5468847A (en) Method of isolating and purifying a biomacromolecule
US4895806A (en) Device for liquid chromatography or immobilized enzyme reaction
US9120037B2 (en) Stackable planar adsorptive devices
US5911883A (en) Flow-by solid phase extraction method
US5863428A (en) Guard cartridge for chromatography
GB2440244A (en) Chromatography column
US20060032816A1 (en) Monolithic structures comprising polymeric fibers for chemical separation by liquid chromatography
US7374673B2 (en) Channeled polymer fibers as stationary/support phases for chemical separation by liquid chromatography and for waste stream clean-up
US5972218A (en) Porous tube filter
CA2137970A1 (en) Cartridge sorption device
KR920007851B1 (en) Chromatography seperating tube
CA1296257C (en) Chromatography column
US20050035044A1 (en) Filter module and device for static filtration of fluids with such a module

Legal Events

Date Code Title Description
MKEX Expiry